AU2005279201B2

AU2005279201B2 - Method for pigment solubilisation, a pigment composition and its use

Info

Publication number: AU2005279201B2
Application number: AU2005279201A
Authority: AU
Inventors: Dennis Selse
Original assignee: Akzo Nobel NV
Current assignee: Akzo Nobel NV
Priority date: 2004-08-31
Filing date: 2005-08-24
Publication date: 2011-08-04
Anticipated expiration: 2025-08-24
Also published as: NO333623B1; EP1786274A1; JP2008511708A; BRPI0515122A; WO2006024620A1; NO20070982L; CA2578903A1; CN101005768A; AU2005279201A1; CN101005768B; MX2007002374A; US20080044538A1

Abstract

The present invention relates to an improved method for solubilising an oil-soluble pigment efficiently in an oil or fat by extraction of a solid preparation containing the oil-soluble pigment, where the extraction takes place in the presence of water, an edible oil or fat and a nonionic surfactant. It also relates to the composition prepared by the extraction, and the use of this composition in animal feed to produce feed pellets. The combination of water and nonionic surfactant increases the amount of pigment that is extracted and solubilised. In detail the process of the invention relates to a method for solubilising an oil- soluble pigment into an oil or fat by extraction of a solid preparation containing the oil-soluble pigment comprising the steps of a) mixing the solid preparation containing the pigment with water, an extraction medium containing an edible oil or fat, and a nonionic surfactant having a hydrocarbyl group, an acyl group or a substituted hydrocarbyl or acyl group containing at least 6 carbon atoms b) optionally centrifugalize the mixture obtained and separate the oil phase. The originally obtained mixture or the separated oil phase may then be added to porous precursor feed pellets to produce feed pellets. These pellets will have a higher amount of oil-soluble pigment available for uptake into the animal.

Description

WO 2006/024620 PCT/EP2005/054145 1 METHOD FOR PIGMENT SOLUBILISATION, A PIGMENT COMPOSITION AND ITS USE The present invention relates to an improved method for solubilising an oil-soluble 5 pigment efficiently in an oil or fat by extraction of a solid preparation containing the oil-soluble pigment, where the extraction takes place in the presence of water, an edible oil or fat and a nonionic surfactant. It also relates to the composition prepared by the extraction, and the use of this composition in animal feed to produce feed pellets. The combination of water and nonionic surfactant increases 10 the amount of pigment that is extracted and solubilised. In animal feed compositions, pigments are often added to endow an appealing colour to the meat or skin of the animals consuming the feed. The pigments used may be natural, synthesized or fermented, and commonly they are oil-soluble. An 15 example of a class of oil-soluble pigments is the carotenoids, e.g. astaxanthin, canthaxanthin and p-carotene. These are insoluble in water, and have a low solubility in organic solvents, fats and oils. Astaxanthin and canthaxanthin are commonly used in fish feed to improve the flesh colour of salmonids, but also give rise to health benefits. Other uses for pigment in animal feed is for the coloration of 20 the skin of some marine warm-water or tropical freshwater fishes, e.g. of the red seabream, and to endow a pink color to the shell and flesh of prawns. In addition to these aqua-cultural uses, the coloring of egg yolks and of the skin of broilers are other feed application areas. 25 Conventional feed pellets are usually formed from a solid base material, which may be protein-based such as fishmeal or carbohydrate-based such as starch, and where the base material is loaded with a fat or an oil component. The fat or oil, that could be either of animal or vegetable origin, is loaded into pores of the precursor feed pellets formed from the base material. The fat or oil increases the 30 energy content of the feed. Other ingredients of the feed are e.g. vitamins, WO 2006/024620 PCT/EP2005/054145 2 minerals, enzymes and the above-mentioned pigments. These latter ingredients, as well as the fat or oil, are preferably added after the pelletizing step, since the oil component interferes with the pelletizing process and many of the pigments lose their activity when heated. Many of the sensitive pigments are available in coated 5 form, e.g. Carophyll@ Pink, which is sold in the form of beadlets. The beadlets of this product consist of a core of astaxanthin emulsified in antioxidants and residing in a matrix of gelatine and carbohydrate, which core is coated by maize starch. The amount of astaxanthin is at least 8% of the beadlet. There is also another astaxanthin product of a similar kind that is called Carophyll@ Pink 10% CWS, 10 which differs from the first-mentioned product only in that the matrix is a lignosulfonate. If these beadlets are added as such to the preformed pellets, most of them are deposited only on the pellets' surface. Especially for aqua-cultural feed this is a disadvantage, since the beadlets will be washed away when the feed comes into contact with water. Also the bioavailability will be less when the 15 pigments are still contained in the beadlets. In EP 839 004-B1 a method is disclosed for loading bioactive ingredients, such as pigments, into feed pellets. The process includes the steps of removing the gelatin and carbohydrate protective shell around the bioactive ingredient enzymatically or 20 by hydrolysis, mixing the uncoated bioactive ingredient with a fat or an oil and loading porous precursor feed pellets with the resulting mixture to produce the feed pellets. In JP7-16075-A a method is described of making a water-soluble pigment solubilised in fat. Firstly polyols are dissolved in water and mixed with the water 25 soluble pigment, and then an oil-phase containing an emulsifier is added to obtain an emulsion of the water-soluble pigment in oil. In JP7-23736-A a method is described of making a carotenoid pigment solubilised in water, where pH is made alkaline, cyclodextrins are mixed to the water and the pigment and finally the pH is restored to neutral.

WO 2006/024620 PCT/EP2005/054145 3 EP 682 874-A2 discloses a bioactive feed pellet, where the bioactive ingredient could be for example a pigment. The bioactive ingredient is applied to the pellet in the form of a primary coating dispersion and/or emulsion and/or solution in a fatty component or a mixture of dietary oil, said component or dietary oil comprises a 5 triglyceride and/or fatty acid thereof having a melting point of above 350C. A second coating layer of an oily product is then applied. In case the bioactive compound to be added is not miscible with the suspending aid, a dispersing or emulsifying agent can be added to improve the mixing properties. Examples of such emulsifiers that are mentioned are distilled monoglycerides, polyunsaturated 10 polyglycerol esters of fatty acids and sorbitan fatty acid esters; saturated monoglycerides are preferred. From the references cited above, it is evident that the extraction of oil-soluble pigments from solid preparations, such as from the above-mentioned beadlets, 15 needs further improvement. Now it has surprisingly been found that when the extraction of a solid preparation, containing an oil-soluble pigment, with a hydrophobic extraction medium, such as an oil or a fat, is performed in the presence of water and a nonionic surfactant, the 20 extraction and solubilisation of the pigment are essentially improved. In detail the process of the invention relates to a method for solubilising an oil soluble pigment into an oil or fat by extraction of a solid preparation containing the oil-soluble pigment comprising the steps of a) mixing the solid preparation containing the pigment with water, an extraction 25 medium containing an edible oil or fat, and a nonionic surfactant having a hydrocarbyl group, an acyl group or a substituted hydrocarbyl or acyl group containing at least 6 carbon atoms, and b) optionally centrifugalize the mixture obtained and separate the oil phase WO 2006/024620 PCT/EP2005/054145 4 This method will lead to a more effective extraction of the pigment from the solid preparation and a more effective solubilisation of the pigment into the oil or fat. The originally obtained mixture or the separated oil phase may then be added to porous precursor feed pellets to produce feed pellets. These pellets will have a 5 higher amount of oil-soluble pigment available for uptake into the animal. One embodiment of the process of the invention, where the solid pigment preparation is a coated pigment, such as a beadlet described above, comprises the following steps: a) the coated pigment is agitated in water at a temperature between 4 and 1000C, 10 and the edible oil or fat comprising the nonionic surfactant is added to the mixture obtained at a temperature of from the melting point of the oil or fat to 100*C with agitation, or the coated pigment and the nonionic surfactant are agitated in water at a temperature between 4 and 100*C, and the edible oil or fat is added with agitation 15 to the pigment-surfactant mixture at a temperature of from the melting point of the oil or fat to 100*C b) optionally the mixture obtained is centrifugalized and the oil phase is separated c) the mixture obtained by step a) or the separated oil phase obtained by step b) is added to porous precursor feed pellets to produce feed pellets. 20 There are several advantages using the method of the present invention. The method is more effective than the prior art methods in extracting and solubilising the pigments, so that a larger proportion of the pigments will be extracted from the solid preparation and will be present in the oil phase. This is demonstrated in the 25 examples, where the method of EP 839 004-B1 to enzymatically, in the presence of water, break down the gelatin and carbohydrate protective shell around the pigment to set it free from a solid preparation (beadlet) is compared to the method of the present invention where the addition of water and a nonionic surfactant more effectively sets the pigment free. Since the extraction and solubilisation of 30 the pigment are more effective, the method of the present invention will lead to a WO 2006/024620 PCT/EP2005/054145 5 higher concentration of pigment in the oil. This will in turn lead to a larger proportion of pigment that is kept in the pellets that are loaded with this oil or fat. Further, the oil-phase is not so easily washed away as the untreated beadlets. Also, there will be a better bioavailability when the pigments are solubilised to a 5 larger extent in the oil (see Bjerkeng, B. et al, Bioavailability of all-E-astaxanthin and Z-isomers of astaxanthin in rainbow trout (Oncorhynchus mykiss), Aquaculture 157, 63-82). The dispersion or oil phase comprises an edible oil or fat, one or more oil-soluble 10 pigments and one or more nonionic surfactants, and the invention also relates to such a composition suitable for use in loading pellets to be used as animal feed. A suitable composition would be an edible oil or fat comprising 0.25-15%, preferably 2-10% and most preferably 4-10% by weight of one or more nonionic surfactants, where the surfactant is an ester, an alkoxylate of an ester or an alkoxylate of an 15 alcohol, preferably a castor oil ethoxylate with 2-40, preferably 2-25 and most preferably 4-20 moles of ethylene oxide, or a diacetyl tartaric acid ester of mono and/or diglycerides; 0.0005 to 1% by weight, preferably 0.0005 to 0.3% by weight, more preferably 0.0005 to 0.2% by weight and most preferably 0.0005 to 0.1% by weight, of one or more oil-soluble pigments; and 0-20% by weight of other 20 components including water. The other components could be vitamins, enzymes, anti-oxidants, residues from the beadlets' gelatine and carbohydrates, minerals, prophylactic agents, pharmacologically active compounds, flavouring agents, preservatives and other common feed additives. The water present in the composition is dissolved or emulsified in the oil by the surfactant, and would 25 normally range between 0.1% and 15% by weight. The edible oil or fat may be a fish-oil, such as menhaden oil, herring oil, sardine oil, tobis oil or capelin oil, hydrogenated fish-oil, castor oil, rapeseed oil, hydrogenated rapeseed oil, corn oil, soybean oil, hydrogenated soybean oil, sun 30 flower oil, hydrogenated sun flower oil, olive oil, hydrogenated olive oil, palm oil, WO 2006/024620 PCT/EP2005/054145 6 hydrogenated palm oil, coconut oil, hydrogenated coconut oil, tallow or lard. Hydrogenated oil is normally needed when the total amount of oil or fat is high, such as for total amounts of oil or fat in fish-feed of 26% (w/w) or higher (counted on the total pellet weight). The amount hydrogenated oil or fat that is present in 5 these pellets is normally between 0.2 to 10% (w/w) of the total amount of oil or fat. The pigment is preferably a carotenoid, which could belong to either of the sub groups carotenes or xanthophylls. Suitable xanthophylls are lutein, zeaxanthin, canthaxanthin, astaxanthin or p-cryptoxanthin, and suitable carotenes are p 10 carotene, alfa-carotene and lycopene. Examples of commercial products containing these pigments are Carophyll@ Pink (Hoffman LaRoche; min 8% (w/w) astaxanthin), Lucantin@ Pink (BASF; min 10% (w/w) astaxanthin), Lucarotin@ 10% Feed (BASF; min 10% (w/w) @ -carotene), Lucantin@ Red (BASF; min 10% canthaxanthin) and Rovimix (Hoffman LaRoche; min 10% (w/w) @-carotene). 15 The surfactant should be a nonionic surfactant, such as an ester, an alkoxylate of an ester or an alkoxylate of an alcohol. Preferred nonionic surfactants are sorbitan esters, ethoxylated sorbitan esters, tartaric acid esters of mono- and diglycerides, alkoxylated fats, oils or other esters, and alkoxylated alcohols. The most preferred 20 nonionic surfactants are castor oil ethoxylates, preferably castor oil ethoxylates with 2-40 moles, more preferably with 2-25 moles, and most preferably with 4-20 moles of ethylene oxide per mol castor oil. Experiments have also been made to use an ionic surfactant, such as a native lecithin, but the results were not as good as when using a nonionic surfactant. Certain nonionics perform better with certain 25 pigments. For example, castor oil ethoxylates are especially suited to be used for the solubilisation of astaxanthin and canthaxanthin, whereas diacetyl tartaric acid esters of mono- and diglycerides are especially suited for the solubilisation of p carotene. A comparison between some castor oil ethoxylates with different amounts of ethylene oxide, and consequently different HLB-values, and the 30 corresponding mixtures of sorbitan monooleate +20EO and sorbitan monooleate WO 2006/024620 PCT/EP2005/054145 7 having the same HLB-values show that the castor oil ethoxylates having up to 25 moles of ethylene oxide are much more efficient in solubilising astaxanthin. The porous precursor feed pellets could be manufactured by any known method, 5 e.g. extrusion, and from any commonly used material, such as carbohydrates or protein. When loading the precursor feed pellets, the temperature should be high enough to keep the fat or oil in a liquid state, but not above the decomposition temperature of the pigment. A suitable temperature is between the melting point of the fat or oil and 600C. The loading of the feed pellets with the pigment-containing 10 oil could be performed by mixing, dipping, spraying, coating or other commonly used means. A suitable pellet composition, obtained by loading precursor feed pellets with the above-mentioned oil or fat composition, has an amount of oil between 1 and 50%, 15 preferably between 3 and 45% and most preferably between 5 and 40%, by weight of the loaded feed pellets. The present invention is further illustrated by the following Examples. 20 Example 1 10% (w/w) of Carophyll@ Pink' was mixed with 90% (w/w) water at a temperature of 600C with stirring. After cooling to room temperature a formulation was made containing 7.5% (w/w) of the mixture and 92.5% (w/w) of a surfactant/fish-oil mixture (sample type A), the formulation was stirred for 2 minutes at a temperature 25 of ca 450C and the next day it was centrifugalized at 5000 rpm (G=34000m/s 2 ) for 5 minutes. A sample was taken with a syringe and filtered through a 0.2 pm micropore filter. If the sample was taken after a few days it was not necessary to centrifugalize the formulation, but the sample could be taken directly from the oil phase and filtered. The sample was then diluted with acetone to a desired 30 concentration, and the absorbance was measured at 474 nm. In Table 1 the WO 2006/024620 PCT/EP2005/054145 8 absorbance values for different samples are displayed, which is a measure of the abilities of the different surfactants to solubilise the pigment astaxanthin. The formulation could also be made by first mixing the surfactant with the pigment/water mixture, and then mix with the fish-oil (sample type B).

WO 2006/024620 PCT/EP2005/054145 9 (D 0 44 C >4 0 Cu 0 -4-, E 0) 4-1 E4-, CUm0~- 0'-0'- '-0(0 0 V 0( cu o o -1 0 0 cu Cu 0 0 0 )C'.,C c 0 o + 8. 0 c ou + 0 _ _ _ - - - - - - - - - - U V0 c 4-1 () 0~~ Cu) E Ecc 0l C)4 1 41 +~ ~ Cu)0 ' 0 cu 0 ) C) ( _ u_0 _ 0 Cu E +C :3 c c 0 0 0 0~~ CU) Cgo Q.. u Q Cu E CUl- mmmm 0 0 Cl)0 0 O U 4- m WO 2006/024620 PCT/EP2005/054145 10 Example 2 The pigment used in this example was Carophyll@ Pink. The procedure followed was the same as for Example 1. 5 The recovery values are based on the assumption that the product Carophyll@ Pink contains 8% astaxanthin, which is the amount astaxanthin that the producer guarantees is present. Absorbance Pigment/ Castor Castor Fish-oil Absorbance at 474 nm Sample water mix oil +6EO oil Tobis at 474 nm after 13 Type (g) (g) +28EO (g) after 1 day 3 days 4 (% (g) recovery) Control 3 37 0.05 0.02 (4.4) A 3 3 34 1.48 0.33 (72.6) A 3 1.5 35.5 1.52 0.3 (66.3) A 3 6 31 1.16 0.2 (43.7) A 3 9 28 1.66 0.22 (47.6) A 3 3 34 1.02 0.2 (44.0) A 3 6 31 0.98 0.19 30.200 m of the oil-phase was diluted with acetone to 10 ml (41.5) 40.400 ml of the oil-phase was diluted with acetone to 100 ml 10 WO 2006/024620 PCT/EP2005/054145 11 The amount of surfactant is not very critical within the investigated range. Sample Pigment/ Castor Castor oil Fish-oil Absorbance Absorbance Type water mix oil +6EO (g) Tobis at 474 nm at 474 nm (g) (g) (g) after 1 day 5 after 23 (% days 6 recovery) A 3 3 34 0.11 A 3 3 34 1.24 0.41 (54.6) (72.2) A 3 1.5 35.5 1.28 0.33 (56.6) (58.3) A 3 0.75 36.25 0.57 0.14 (25.2) (24.8) A 3 0.375 36.625 0.14 0.05 _(6.2) (8.9) A 1.5 3 35.5 0.72 0.22 (66.0) (80.6) 60.200 m of the oil-phase was diluted with acetone to 10 ml 60.500 ml of the oil-phase was diluted with acetone to 100 ml 5 *for an absorbance value of >0.9 there is not a linear relationship between absorbance and concentration Within this range there is a correlation between the amount of surfactant used and the amount of pigment solubilised. 10 Example 3 In this experiment the amount of pigment to be solubilised is varied from ca 25 ppm, counted on the whole mixture, up to 750 ppm, and the amount of surfactant (castor oil +6EO) used is also varied. 15 5-10% (w/w) of Lucantin@ Pink CWD was mixed with 95-90% (w/w) of water at room temperature with stirring. A formulation was made containing ca 0.5-7.5% (w/w) of the mixture and ca 99.5-92.5% (w/w) of the surfactant/fish-oil mixture. The formulation was stirred for 2 minutes at a temperature of 450C and then WO 2006/024620 PCT/EP2005/054145 12 centrifugalised at 5000 rpm for 5 minutes. The sample was filtered through a 0.2pm micropore filter and 0.400 ml of the filtrate was diluted with acetone to 100 ml. Weight Pigment/ Pigment Castor Fish-oil Absorbance Sample ratio water mix concentra- oil Tobis at 474 nma type surfactant (g) tion +6EO (g) (% /oil (ppm) (g) recovery)' Control 0 0 0 37 0.015 Only oil 0/100 0.19 26 0 37 0.031a A 2/98 0.18 24 0.75 36.25 0.032a (102.2) A 8/92 0.17 23 3 34 0.029a (94.5) A 16/84 0.18 24 6 31 0.032a (113.0) Only oil 0/100 0.5 133 0 37 0.015" (0%) A 2/98 0.51 136 0.75 36.25 0.1070 (96.2) A 8/92 0.5 133 3 34 0.107D (98.5) A 16/84 0.5 133 6 31 0.098" (89.5) Control 0 0 0 37 0.013 Only oil 0/100 2.432 750 0 30 0.018a (0.9) A 2/98 3 750 0.75 36.25 0.103a (16.0) A 8/92 3 750 3 34 0.515a (88.6) A 16/84 3 750 6 31 0.479a (81.8) aafter 4 days in refrigerator 5 direct measurement The absorbance values have been corrected for the absorbance of the oil itself, without added pigment.

WO 2006/024620 PCT/EP2005/054145 13 'The recovery values are based on the assumption that the product Lucantin@ Pink CWD contains 10% astaxanthin, which is the amount astaxanthin that the producer guarantees is present. 5 This experiment shows that for the amounts 23-136 ppm of pigment, the whole amount is easily solubilised even at the low weight ratio of 2/98 of surfactant to oil, whereas for the higher amount of 750 ppm a higher weight ratio is required. However, a weight ratio above 8/92 does not result in any increase of the amount of pigment solubilised. 10 Example 4 The procedure followed was the same as for Example 1. Absorbance at 474 Sample Pigment Pigment/water Castor oil Fish-oil nm after 1 day in type mix +6EO Tobis refrigerator and (g) (g) (g) filtration 4 (% recovery) Control Lucantin@ 3 37 0.018 Pink (3.2) CWD A Lucantin@ 3 3 34 0.522 Pink (91.9) CWD A Lucantin@ 2 3 34 0.362 Pink (95.6) CWD A Lucantin@ 1 3 34 0.164 Pink (86.6) CWD A Lucantin@ 0.5 3 34 0.107 Pink (113.1) CWD A Lucantin@ 0.25 3 34 0.063 Pink (133.1) CWD 0.400 Il of the oil-phase was diluted with acetone to 100 ml WO 2006/024620 PCT/EP2005/054145 14 Lucantin@ Pink CWD is a product produced by BASF that contains at least 10% (w/w) of the pigment astaxanthin. The recovery values are based on this amount of pigment in the product. 5 Example 5 In this example the castor oil ethoxylates are compared to other kinds of surfactants. The pigment used was Carophyll@ Pink. The procedure followed was 10 the same as for Example 1.

WO 2006/024620 PCT/EP2005/054145 15 (D (D0 cu V> 9TCO LO~4O qT0 - Mr-Loo M 00 CU) -4-1 U) 0 4--4-, 00 U) 0 + (D C C 4-1u -4 'a ~U) 0 0 (D c

I.

C) 0U 0 E cO cC UL ) C.u C Cu flCu E: C0 0o. _ "l U) .) cu 0 ' C U Cu CN~~U (M Cf x 0U + 0 -1-. cu c 0 0V c 0 +U cu CD Cu =0 +4- 4 ~ L.uC x 0 . ) _ Cu4- _r_ 0l (C WO 2006/024620 PCT/EP2005/054145 16 Example 6 In this example the effect of HLB-values on the solubilising ability is investigated for castor oil ethoxylates and for Tween 808/Span 809 mixtures having the same 5 HLB-values as the castor oil ethoxylates. The pigment used was Lucantin@ Pink CWD and the oil was Tobis fish-oil. The procedure was the same as in Example 1 except that the pigment was mixed and stirred with the water at room temperature. All samples were of type A. The formulations contained 2g of the specific surfactant or surfactant mixture, and the weight ratio surfactant:fish-oil was 6:94. 10 The amount of pigment/water mix was 2.57 g. Absorbance at Absorbance at Castor oil 474 nml" for 474 nml" for the ethoxylate the castor oil Tween80/Span8O Tween80/Span8O HLB- number of ethoxylates mixtures mixtures value EO units (% recovery) (g/g) (% recovery) 5.9 6 0.464 0.3/1.7 0.109 (82.6) (19.2) 9.4 15 0.498 0.954/1.046 0.167 (88.7) (29.7) 10.5 20 0.424 1.196/0.804 0.218 (75.5) (38.8) 11.8 25 0.261 1.384/0.616 0.244 (46.5) (43.5) 13.3 36 0.17 1.682/0.318 0.218 (30.3) (38.8) 'Tween ;o is sorbitan monooleate +20EO 9 Span 80 is sorbitan monooleate 100.200 ml of the filtered oil-phase was diluted with acetone to 10 ml.

WO 2006/024620 PCT/EP2005/054145 17 The samples were then further diluted by taking 2.00 ml of the acetone solution and dilute it to 10 ml. 5 For the castor oil ethoxylates there is a marked decline in the solubilising ability around a HLB-value of 11, whereas for the Tween 80/Span 80 mixtures the level is about the same for all mixtures and generally lower than for the castor oil ethoxylates. However, both types of compounds have an effect on the solubilisation of the pigment astaxanthin. 10 WO 2006/024620 PCT/EP2005/054145 18 -cf -4-1 (D (D C.) v l x C0 C : 0~0 0 C: 0' C )( tDt 4-1 c. 4' C .J O - a) 0 U- 0C)C N0 M Cu CL u U)C. a)x ~ 0 0 0 0 0 0or- o L o 'a V) " 4-j ocu c-) EWN .mD0 V t C I. Cu cu WE CE Cu C) C-.' C) NCN a) CDam <Q0 Cu ~a -,-j4j 44- a) E 00 a) cn C COL ~~ Cu a)Cu 2 0 E~ mc C C D r- r- r - Cu a.-

N

-4-j CD C a)0 a) 0. ' . 0O O C 0 LU EM CN DCN (= 2- Cu W<0.0 WO 2006/024620 PCT/EP2005/054145 19 0 E N C: Lo - CU C) CC Cu:L : Cu 70 U, U , ( 0 0 0 .2 E2 0 Cu c CN 0 . c CU C IU 1 4-1 (10 0 _r EN C 400 0O 4 u - - . a I.- " z C 0 oc :) Cu C EN a m' Cu C)' C Cua m 4-1 a 0 6 -. a' 00' C) 0 ~~i< E~a r- ~ ~ ~ 4 LLr ~~ C l O > ~E a'w 0C~~( -- r 0 CuTCu.~eu. U)I 2 L0 0 a'C 2C U)OC C Cu C C o~~ 0J- - _O _O 'tO <- C WO 2006/024620 PCT/EP2005/054145 20 4-1 - nE 0- 0 (1 C L -1 C.u -' (D 0CT ( C0Eu 0 6666 u) 2 :)CC o 1- ' C -a - U DC D D ( CCu "t Cc-4-1 U)0 (D 0)- (DU E) -4-,C) C ) C ) o Cc CI CO C CO O C U)) Cu U) 4- N c2 m U) UD) Q. U) U) 0 WD C , Dx +C CuN E U) CU + 0 E = m)~ _D 00.4' CU ,C ~ ' 4CC)CDC 0c . N ND C) -4-' -4-1 '4-1 C c U) x LUco -D4-1,oCN( E~u Cu Xgo C. ___ -4- 4-, 0 C ) + U, -F. 0- U) =)U2~U-U2 C C u E CO' cm C Cu C C C a) CU8LD

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WO 2006/024620 PCT/EP2005/054145 21 - ~ !E E U) Cu U,) U) C. CuV00 c)C' cI LOC L'LO ,t o6 N E c'~ (D 4 0D C)O -4- . 0 C CD T) __ '4-1 c 0 a) cm CO CO) Cu f) C) Q. _) N .) 0 0 4C1 0 0 L (D C Cu 00 !E 0 _ 0O 0 4-14-,C CI) CD (DO N a.) N mC co-) 0 -4-, 4 0 N C) D - -1. O LO L O L c am CO C N- N- N- N- N -2 E :3 CU C E Cu cu cu cu 0 0 LL OcM WO 2006/024620 PCT/EP2005/054145 22 (D '4 0 0E (N CC N00 L ) 00 9T 000 c) 0i66 clc6 c N 0 0 CD 0(D C') -~ E (D .0 C) C) C)( -4- -4 c ~C (D c Q.4- C 0 CNC (D) -4-' C) 0 00 CN 0 U)) -~ Cu EE C) = _U I - I.__ : :- m4-' 1 0D2 -4- QI N~ 0 C Cl rl CN1 __ O co LO0 0 0 Cu N C, COC ( U 0 0E CO 0 ~ U U C) c 00 C.) - Na ) C CO 0 WO 2006/024620 PCT/EP2005/054145 23 D N .c E -0-C U) CU m O r-- r 'a. 0 00 1 ) 1L q )1 CO CCCuC 0 0- 0 C U) r_ _ __ U) CL -C 4--4-, Cm 0 U) Cf) C') U') Cf) E CC a) LL~' C E 0 c: vl -J -0 .C U E M a) -I-, m - U -2 *c 0) C)-~0 0 o)C o. = CCN 4 U 1 x 0 co+ C > U) . )0> 1 I.- EC 0 ' 40 (D 0 xE ( OD5~ 0 W (D QW.

0 wMM N CD 0 CU)0 0~ Cc (D _r_ U) "- 4 06 0 -0 N NM ' U) C) 4-j + __ C Cu (D - 0 (D Cmu C.) -Cu Cu 0 C2~ . -a um t- 0 NmR 0 (3 o +F C ~E (D Cu U)E U) r- 4 = ( (DC U)

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(D* a) U) (Dx CU 4- 4, - (~ -- U (D IU U 0~0 c _r_ X c -r - I- U) WO 2006/024620 PCT/EP2005/054145 24 E -0 c -4,C Cl) _ ) 4N 00 Cl) M 00 cc 0) vl O 0 C) C '4-1 CuC a) ~ U r_ _ ___ Q~ ~0-4

~

4 1 i) !E 0 (D ___ E 4-) U 0 0 M - U) I. 0 0 c-c 0 0 + 2:C 0D -00 4C 0- 0.C C +Cu. a) m U E DD ____ __ __ 4-1 4) 0) 0 0 U)CDC C + WO 2006/024620 PCT/EP2005/054145 25 E -0 LO U)Er SCUc C0 N N 1- U'O 0 Cu-u0 ccC)v- C0 0) m~ (D ,)L N U'O C)~ c 4 o cm = CO LOU a,- ______ 0 0 C.u co U'- :- (M C) C') U') U') U') -4-4-1 EE 0 V( 0. Lta, 4C a, ( (D C _ _ _ _ CMC 0 U CO 0 75 *O m a, Cu C I.

'a 0COoCDC C) ~~4-1, '4-4-1 o 0 0 WLOCD NN 40 4o ) O N -- 4-1 4o o a, _ _ _ _ 00-C m C 4 -a, E 0D =L E -4- 44-, E) E m c5 f o c a, 44-N1 a, 4-~ 04C E (Cu( a, 0, 0 , , 0 (D t m .) C. C) .) C.Cu :3u C) :3 a,: ): C 3C (D _ V-- _j V- _j V-- V- _j - CD WO 2006/024620 PCT/EP2005/054145 26 E 1 U)LOU L -- '0 CC 0 C C C .0 U) 4M, flkr LO LO LO LO LO Cl) 0l l l l E ~o Q u w (D M- o N., 00+0 4-I E (D 0 CU CU ( 0 0 75 U) E 4U, U) 0D 0 flU). N( U), 0 U)- U)( (D -' 0. L- 0 Cu 0 -c 4 _ -4-, C CN E =0 (D - 0W U 4 -0 U C CN E C Cu CD u + l Cl) 0 m x Cl, U 4)C- Cn Cf) Cf C C 0 C __u_ WO 2006/024620 PCT/EP2005/054145 27

I.

c 0 E 0 C 4-1 C cc C C > Na). C. Cu Cf M0DM M MT-M M ( = 0 0 cm 0 4-Q 00 U, 0 Q. -E _ _ _ _ 0 a.) C) a) 0, ' ~ C Cf) Cf) Cf (D CN E (D 4-1-' CUa . o :)C) x E a) T- a 0 0 E 00 .) a)+ CuCu 0 0 "t >D Cu mO

(D

CD 4__1 ==UC 0 a) Cu .0C E m +) E m Cfl C) Cf f)a) 4-1 Cucu 4'4 0D E m0~ c 0Ca -~~~( 0CC C C C U Cu Q'. (D m C X E) 0 Cu- c m WO 2006/024620 PCT/EP2005/054145 28 Example 11 In this example a comparison is made with the enzymatic method described in the prior art. The procedure for the enzymatic method was the following: 10% (w/w) of Lucantin@ Pink was mixed with water, that was buffered to pH 7.5 5 and that contained 0.5 mg/ml protease (Protease Streptomyces griseus; CAS number 9036-06-0, 5.6 units/mg solid powder), at a temperature of 550C with stirring. The pigment/water/enzyme mixture was then stirred at 450C for 90 minutes. After cooling to room temperature a formulation was made containing 7.4%(w/w) of the mixture and 92.6%(w/w) of fish-oil, the formulation was stirred for 10 2 minutes at a temperature of ca 450C and the next day it was centrifugalized at 5000 rpm (G=34000m/s 2 ) for 5 minutes. A sample was taken with a syringe and filtered through a 0.2 pm micropore filter. 0.400 ml of the filtrated sample was then diluted with acetone to 100 ml, and the absorbance was measured at 474 nm. The sample according to the invention was treated in the same manner, except that it 15 contained no protease and the formulation was made by mixing with 92.6% (w/w) of castor oil +6EO/fish-oil mixture. In Table below the absorbance values for the different samples are displayed, which is a measure of the abilities of the different methods to solubilise the pigment astaxanthin. Absorbance at 474 nm Pigment/water Castor oil Fish oil after 2 days Sample mix +6EO Tobis in refrigerator Type Pigment (g) (g) (g) and filtration Control Lucantin@ 3 37 0.025 Pink A Lucantin@ 3 2 35 0.589 Pink Comparison Lucantin@ 3 37 0.099 (protease 24 ) Pink 24The protease is active at temperatures between 25 to 700C and at pH-values 20 between 7.0 and 10.0.

WO 2006/024620 PCT/EP2005/054145 29 The comparison reveals that much more astaxanthin can be solubilised by using the method of the present invention than by using the enzymatic procedure disclosed in the prior art. 5 Example 12 This example is also a comparison with the enzymatic method described in the prior art. The procedure was the same as in Example 11, except that the water was buffered at pH 9.5 and contained 1.0 mg/ml or 0.35 mg/ml of a protease (Protex 6L produced by Genencor International; activity 580000 DU/g) Absorbance at 474 nm Pigment/water Castor oil Fish oil after 3 days Sample mix +6EO Tobis in refrigerator Type Pigment (g) (g) (g) and filtration A Lucantin@ 3 2 35 0.603 Pink Comparison Lucantin@ 3 37 0.016 (protease 24 Pink 0.35 mg/ml) Comparison Lucantin@ 3 37 0.046 (protease 24 Pink 1.0 mg/ml) A + Lucantin@ 3 2 35 0.567 protease Pink (1.0 mg/ml) 10 24The protease is active at temperatures between 25 to 70*C and at pH-values between 7.0 and 10.0. The comparison reveals that also during these conditions with a higher pH, a different protease and a higher concentration of the protease, much more 15 astaxanthin can be solubilised by using the method of the present invention than by using the enzymatic procedure disclosed in the prior art.

Claims

1. A method for solubilising an oil-soluble pigment, which is a carotenoid, into an oil or fat by extraction of a solid preparation containing the oil-soluble pigment, 5 comprising the steps of a) mixing the solid preparation containing the pigment with water, an extraction medium containing an edible oil or fat, and a nonionic surfactant selected from the group consisting of a castor oil ethoxylate with 2 to 25 moles of ethylene oxide and a diacetyl tartaric acid ester of mono- and/or diglycerides. 10 b) optionally centrifugalize the mixture obtained and separate the oil phase

2. A method according to claim I where the solid preparation containing the pigment is a coated pigment and a) the coated pigment is agitated in water at a temperature between 4 and I 00 0 C, and the edible oil or fat comprising the nonionic surfactant is added to the mixture 15 obtained at a temperature of from the melting point of the oil or fat to I 00 0 C with agitation, or the coated pigment and the nonionic surfactant are agitated in water at a temperature between 4 and I 00*C, and the edible oil or fat is added with agitation to the pigment-surfactant mixture at a temperature of from the melting point of the oil or fat to 20 100*C

3. A method according to claim Ito 2 where the pigment is selected from the group astaxanthin, canthaxanthin and p-carotene.

4. An edible oil or fat composition comprising 0.25 to 15% by weight of one or more nonionic surfactants -selected from the group consisting of a castor oil 25 ethoxylate with 2 to 25 moles of ethylene oxide and a diacetyl tartaric acid ester of mono and/or diglycerides, 0.0005 to 1% by weight of one or more oil-soluble carotenoid pigments, and Oto 20% by weight of other components including water.

5. A composition according to claim -4 where the oil is selected from the group castor oil, a fish-oil, rapeseed oil, corn oil and soybean oil. 30

6. A method for producing feed pellets by adding the composition comprising one or more solubilised oil-soluble carotenoid pigments as defined in claim -4 to5 to porous precursor feed pellets. 31

7. Use of a nonionic surfactant, where the surfactant is a castor oil ethoxylate with 2 to 25 moles of ethylene oxide or a diacetyl tartaric acid ester of mono and/or diglycerides, as a solubiliser, for an oil-soluble carotenoid pigment in an edible oil in the method of claim 1. 5

8. Use of the composition according to any one of claims - 4 to 5 for the production of pellets for animal feed.

9. A pellet composition characterized in that it has been obtained by loading a composition according to any one of claims -4 to 5 to precursor feed pellets, and where the amount of oil is 1 to 50% by weight of the loaded feed pellets.

10 10. A method for solubilisation an oil-soluble pigment, said method according to claim I and substantially as hereinbefore described with reference to any one of the examples.

11. An oil-soluble pigment obtained by the method of any one of claims I to 3 and 10. 15 Dated 27 June, 2011 Akzo Nobel N.V. Patent Attorneys for the Applicant/Nominated Person SPRUSON & FERGUSON